Acetaldehyde Production by Ethanol Dehydrogenation
Background
Acetaldehyde is a colorless liquid with a pungent, fruity odor. It is primarily used
as a chemical intermediate, principally for the production of acetic acid, pyridine and
pyridine bases, peracetic acid, pentaeythritol, butylene glycol, and chloral. Acetaldehyde
is a volatile and flammable liquid that is miscible in water, alcohol, ether, benzene,
gasoline, and other common organic solvents. The goal of this project is to design a
grass-roots facility that is capable of producing 95,000 tons of acetaldehyde per year by
ethanol dehydrogenation.
Process Description
A preliminary base case BFD for the overall process is shown in Figure 1.
Unit 100
A PFD of Unit 100 is shown in Figure 2. Ethanol, an 85-wt.% solution in water,
Stream 1, is combined with 85-wt.% ethanol recycle stream, Stream 23, from Unit 200.
The resultant stream, Stream 2, is then pumped to 100 psia and heated to 626°F in E-101
and E-102 before being fed to R-101, an isothermal, catalytic, packed-bed reactor, where
the ethanol is dehydrogenated to form acetaldehyde. The reactor effluent is then cooled
in E-103 and E-104. The resultant two-phase stream, Stream 8, is then separated in V101. The vapor, Stream 9, is sent to T-101 where it is contacted with water, which
absorbs the acetaldehyde and ethanol from the vapor stream.
The resulting vapor
effluent, Stream 11, is then sent for further processing and recovery of valuable
2
hydrogen. Alternatively, this stream could be used as fuel. Stream 12, the liquid, is
combined with Stream 14, the liquid effluent from V-101, and sent to Unit 200.
Unit 200
A PFD for Unit 200 is shown in Figure 3. Stream 15 enters T-201 where the
crude acetaldehyde, Stream 16, exits as the distillate. This crude acetaldehyde is then
sent to T-203 where the acetaldehyde is purified to 99.9-wt.%, Stream 17. The bottoms,
Stream 18, is sent to waste treatment. The bottoms from T-201, Stream 19, is sent to T202 to begin the purification process of ethanol. In T-202, ethyl acetate and some water
is removed from Stream 19 and exits as the distillate, Stream 20, which is then sent to
waste treatment. The bottoms, Stream 21, is sent to T-204 where ethanol is separated
from butanol, ethyl acetate, and most of the water. These impurities exit in Stream 22
and are sent to waste treatment. The distillate consists of an 85-wt.% solution of ethanol,
which is then recycled back to Unit 100 to be used in the feed. Waste streams, Streams
18, 20, and 22, all contain small quantities of valuable chemicals. Methods for their
separation and purification should be investigated.
Necessary Information and Simulation Hints
The following reactions occur during the dehydrogenation of ethanol:
CH 3CH 2OH → CH 3CHO + H 2
(1)
2CH 3CH 2OH → CH 3COOC2 H 5 + 2 H 2
(2)
2CH 3CH 2OH → CH 3 (CH 2 )3 OH + H 2O
(3)
CH 3CH 2OH + H 2O → CH 3COOH + 2H 2
(4)
The conversion of ethanol is assumed to be 60.8%. The yields for each reaction are as
follows:
3
(1)
acetaldehyde 91.7%
(2)
ethyl acetate 3.8%
(3)
butanol 2.4%
(4)
acetic acid 2.1%
References are not available for these values. Since reaction kinetics were not
available, the above conversions were assumed in the design of the process.
NRTL thermodynamics was used for K-values, as suggested by the Chemcad
expert system.
Equipment Summary
E-101
Reactor Preheater
E-102
Reactor Preheater
E-103
Heat Exchanger
E-104
Heat Exchanger
E-105
Heat Exchanger
E-201
Condenser
E-202
Reboiler
E-203
Condenser
E-204
Reboiler
E-205
Condenser
E-206
Reboiler
E-207
Condenser
E-208
Reboiler
H-101
Fired Heater
4
P-101A/B
Feed Pump
P-102A/B
Dowtherm A Pump
P-201A/B
Reflux Pump
P-202A/B
Reflux Pump
P-203A/B
Reflux Pump
P-204A/B
Reflux Pump
T-101
Absorber
T-201
Distillation Column
T-202
Distillation Column
T-203
Distillation Column
T-204
Distillation Column
V-101
Flash Vessel
V-201
Reflux Vessel
V-202
Reflux Vessel
V-203
Reflux Vessel
V-204
Reflux Vessel
5
Stream Tables
Stream
1
2
3
4
5
6
Temp. (°F)
107.6 166.0 166.6 382.8 626.0 626.0
Press. (psia)
14.7
14.7
100
96.2
96.2
96.2
Vapor Fraction
0.0
0.0
0.0
1.0
1.0
1.0
Total Flow (lbmol/h)
1037.9 1498.7 1498.7 1498.7 1498.7 2076.0
Component Flows (lbmol/h)
Acetaldehyde
-2.4
2.4
2.4
2.4 546.6
Acetic Acid
-----11.8
Butanol
-2.3
2.3
2.3
2.3
15.8
Water
336.8 464.6 464.6 464.6 464.6 466.3
Ethanol
701.1 1028.9 1028.9 1028.9 1028.9 403.3
Ethyl Acetate
-0.4
0.4
0.4
0.4
21.7
Hydrogen
-----610.4
Stream
7
8
Temp. (°F)
387.9 157.0
Press. (psia)
96.1
95.1
Vapor Fraction
1.0
0.4
Total Flow (lbmol/h)
2076.0 2076.0
Component Flows (lbmol/h)
Acetaldehyde
546.6 546.6
Acetic Acid
11.8
11.8
Butanol
15.8
15.8
Water
466.3 466.3
Ethanol
403.3 403.3
Ethyl Acetate
21.7
21.7
Hydrogen
610.4 610.4
9
10
107.3 152.3
94.3
94.3
1.0
0.0
683.6 3600.1
63.4
-----5.7 3600.1
3.2
-0.9
-610.4
--
11
12
152.6 152.2
94.3
94.3
1.0
0.0
638.1 3645.7
0.9
62.5
----26.9 3578.9
-3.2
0.2
0.7
610.4
0.2
6
Stream
13
14
15
Temp. (°F)
107.3 209.0 173.8
Press. (psia)
94.3
94.3
94.3
Vapor Fraction
0.0
0.0
0.0
Total Flow (lbmol/h)
1392.4 1392.4 5037.7
Component Flows (lbmol/h)
Acetaldehyde
483.2 483.2 545.7
Acetic Acid
11.7
11.7
11.8
Butanol
15.8
15.8
15.8
Water
460.6 460.6 4039.5
Ethanol
400.1 400.1 403.3
Ethyl Acetate
20.8
20.8
21.5
Hydrogen
----
Stream
19
Temp. (°F)
293.4
Press. (psia)
94.3
Vapor Fraction
0.0
Total Flow (lbmol/h)
4435.1
Component Flows (lbmol/h)
Acetaldehyde
2.4
Acetic Acid
11.7
Butanol
15.8
Water
3985.0
Ethanol
400.9
Ethyl Acetate
19.4
Hydrogen
--
16
190.1
94.3
0.0
603.5
17
184.5
94.3
0.0
539.0
18
259.9
94.3
0.0
64.6
543.2
-0.1
55.6
2.5
2.2
--
537.7
--1.2
----
5.4
20
21
22
267.2 297.4 315.1
94.3
94.3
94.3
0.0
0.0
0.0
54.3 4380.7 3920.0
23
274.9
94.3
0.0
460.7
-2.4
--11.7
11.7
-15.8
13.4
11.3 3973.7 3845.8
24.1 376.8
49.0
19.0
0.4
-----
2.4
-2.4
127.9
327.8
0.4
--
-0.1
54.4
2.4
2.1
--